Agriculture is the backbone of Ghana’s economy, predominantly characterized by crop production. Different food and cash crops are cultivated, providing substantial biomass to promote Ghana’s circular bioeconomy when comprehensively utilized. The study focused on the selection of major crops cultivated in Ghana. Given this, 12 major crops were selected from 2011 to 2020 from the database of the Food and Agricultural Organization (FAO) [21] . Agricultural residues were traditionally utilized as fertilizer, animal feed, cooking fuels and used in landfills to check erosion [22] . Due to numerous constraints, not all agricultural residues can be collected and reused [23] . This means that only a fraction of residues are converted into bioenergy [24] . In addition, a critical factor that could affect the annual agricultural residue supply is the recoverable proportion [25] . The current study determined the collectible agricultural residue potential based on Equation (1).

$A{R}_P\left(j\right)={\displaystyle {\sum }_{i=1}^n\left(P_P\left(i,j\right)\times P_{RPR}\left(i,j\right)\times C_f\left(i,j\right)\right)}$ (1)

where $A{R}_P\left(j\right)$ is the collectible agricultural residues (tonnes); $P_P$ is the crop produced; $P_{RPR}$ is the residue-to-product ratio and $C_f\left(i,j\right)$ is the residue collectible fraction retrieved from Kemausour et al. [23] .

Agricultural residues are rich in potassium (K), carbon (C), nitrogen (N) and phosphorus (P) which are used to produce a variety of bioenergy sources [26] [27] . The anaerobic digestion (AD) technology can generate renewable energy in the forms of biogas and bio-methane from residues. When residues are used as a feedstock for biogas production, 25% - 55% carbon dioxide (CO₂) and 40% - 75.7% methane (CH₄) can be produced [28] [29] . Estimating the biogas digester’s capacity is critical for designing an efficient biogas steam reforming process. The ability of the digester to produce biogas is determined using a theoretical approach. Buswell’s equation was used to determine the potential yield of biogas from the feedstock. The mineral composition of residues was used to determine the stoichiometry of feedstock degradation [17] , as shown in Equations (2) and (3).

$\begin{array}{l}{\text{C}}_q{\text{H}}_r{\text{O}}_s{\text{N}}_t+\left(q-\frac{r}{4}-\frac{s}{2}+\frac{3t}{4}\right){\text{H}}_{\text{2}}\text{O}\\ \Rightarrow \left(\frac{q}{2}-\frac{r}{8}-\frac{s}{4}+\frac{3t}{8}\right){\text{CO}}_2+\left(\frac{q}{2}+\frac{r}{8}-\frac{s}{4}-\frac{3t}{8}\right){\text{CH}}_4+t{\text{NH}}_{\text{3}}\end{array}$ (2)

${\text{C}}_q{\text{H}}_r{\text{O}}_s{\text{N}}_t+Z_1{\text{H}}_{\text{2}}\text{O}\Rightarrow Z_2{\text{CO}}_{\text{2}}+Z_3{\text{CH}}_4+Z_4{\text{NH}}_3$ (3)

The variables q, t, s, r were the number of carbon (C), nitrogen (N), oxygen (O), and hydrogen (H), atoms, respectively and was estimated using Equation (4).

$M_{ratio}=\frac{U_A}{M_m}\times \frac{1}{N_{M_r}}$ (4)

$U_A$ is the C, N, O and H of agricultural residues obtained from various literatures; $M_m$ is the molar mass of C, N, O and H [30] and $N_{M_r}$ is the N mole ratio.

Biogas ( $B{G}_{\left(p\right)}$) potential was estimated in Equation (5).

$B{G}_{\left(p\right)}=P_{C{O}_2}+P_{C{H}_4}$ (5)

$P_{C{O}_2}$ and $P_{C{H}_4}$ are the CO₂ and CH₄ potential of the biogas at a standard temperature (0°C) and pressure (1 atm) expressed in m³/tonne. The $P_{C{H}_4}$ and $P_{C{O}_2}$ were determined based on Equations (6) and (7) [17] .

$T_{C{H}_4}=22400\times \frac{\frac{q}{2}+\frac{r}{8}-\frac{s}{4}-\frac{3t}{8}}{12q+r+16s+14t}$ (6)

$T_{C{O}_2}=22400\times \frac{\frac{q}{2}-\frac{r}{8}+\frac{s}{4}+\frac{3t}{8}}{12q+r+16s+14t}$ (7)

During anaerobic digestion technology, about 10% of the feedstock (agri-wastes) fails to decompose in the digester [30] and about 5% to 10% of residues synthesizes the cell tissues of the microorganisms that aid in microbial

decomposition [17] . The estimation of the actual biogas ( $B{G}_{\left(Actual\right)}$) potential was based on Equation (8).

$B{G}_{\left(Actual\right)}=A{R}_P\left(j\right)\times B{G}_{\left(p\right)}\times \omega$ (8)

where ω is 85% which represents the portion of residues used for cell tissue synthesis [31] .

Before it can be used in the reforming process, the raw biogas must undergo purification and augmentation [32] . Chemically, pure biogas consists of about 93% - 96% CH₄, H₂S (<20 ppm) and 4% - 7% CO₂ [33] . Given this, the study assumed CO₂ is the only pollutant present in purified biogas and the determination of the volume of CH₄ was based on [34] , as shown in Equation (9).

$C{H}_{4_{\left(Pure\right)}}=B{G}_{\left(Actual\right)}\times \beta \%$ (9).

$\beta \%$ is a biogas upgrading percentage taken as 75.7% [29] .

Steam reforming is a common method for producing hydrogen, which requires operating at high temperatures to get a high hydrogen yield [15] . The steam methane reforming (SMR) process, which has a conversion efficiency of between 74% and 85%, is the most widely used and technologically advanced technique for producing hydrogen [35] . The biogas steam reforming process produces half the hydrogen generated globally [29] . During the steam reforming of biogas, the three significant reactions below occurs (Equation (10) to Equation (12)) [15] :

steam reforming (SR)

${\text{CH}}_4+{\text{H}}_{\text{2}}\text{O}\rightleftharpoons \text{CO}+3{\text{H}}_2\Delta H_{298}^0=+206.2\text{kJ}/\text{mol}$ (10)

water gas shift (WGS)

$\text{CO}+{\text{H}}_{\text{2}}\text{O}\rightleftharpoons {\text{CO}}_2+{\text{H}}_2\Delta H_{298}^0=-41\text{kJ}/\text{mol}$ (11)

and dry reforming (DR)

${\text{CH}}_4+{\text{CO}}_2\rightleftharpoons {\text{CO}}_2+4{\text{H}}_2\Delta H_{298}^0=+247.9\text{kJ}/\text{mol}$ (12)

Dry reforming can be disregarded when there is a significant concentration of steam during the reforming process [15] , and the efficiency of the reform reactors determines how much hydrogen is produced. The potential for producing large amounts of hydrogen was determined analytically using the stoichiometric chemical equations of these reactions. From Equation (12), one kilogram of steam-reformed methane yields 0.5 kg H₂ gas. The study assumed that the reformer derives all of its energy from a biogas-fueled boiler. The H₂ produced depends on the system’s reformer and boiler efficiency. Therefore, the Hydrogen

( $H_{2_{\left(Q\right)}}$) produced from biogas steam reforming was determined based on Equation (13) [17] .

$H_{2_{\left(Q\right)}}=C{H}_{4_{\left(Pure\right)}}\times densit{y}_{\left(C{H}_4\right)}\times 0.5\times {\eta }_{\left(sys.eff.\right)}$ (13)

where $densit{y}_{\left(C{H}_4\right)}$ is the density of CH₄; ${\eta }_{\left(sys.eff.\right)}$ denotes the efficiency of the

reformer and boiler as 80% [29] .

The measurement of the energy content of hydrogen derived from biogas steam reforming was conducted by assessing its electricity generation capacity. In this study, the energy content of bio-H₂ was determined only by its capacity to generate electricity for various applications. One of the many applications for hydrogen’s outstanding energy carrier capabilities is the production of energy [36] which is one of the most environmentally friendly ways to produce electricity [37] . Biomass-based hydrogen production has emerged as a promising electricity potential [38] . In addition, utilizing biomass waste for energy production has significant environmental benefits and achieves an excellent 94.33% ecological efficiency rating. Hydrogen production and its electricity potential positively correlate with steam reforming efficiency and the biomass waste collection rate

[17] . The hydrogen-electricity potential ( $H_{2_{\left(Elec.\right)}}$) was determined based on Equation (14).

$H_{2_{\left(Elec.\right)}}=\delta \times LH{V}_{\left(hydrogen\right)}\times densit{y}_{\left(H_2\right)}\times H_{2_{\left(Q\right)}}$ (14)

where δ represents the fuel cells electricity conversion rate (taken as 60%) from

Alves et al. [33] ; $LH{V}_{\left(hydrogen\right)}$ represents H₂ lower heating value (LHV) which is 33.3 kWh [39] and $densit{y}_{\left(H_2\right)}$ is the density of hydrogen considered as 0.09 kg/m³ [17] .

The parameters used to determine the H₂ costs are the project’s operations and maintenance cost, the initial cost of investing in the biogas steam reformer, boiler and other variables. The estimation of hydrogen cost was based on Equation (15) to Equation (20).

$Cos{t}_{H_2}=M_{Cost}+\frac{I_{cost}\times F}{hrs\times H_{2_{\left(Elec.\right)}}}+P{n}_{cost}$ (15)

$P_{cost}=\frac{P{o}_{bio}\times Bi{o}_{cost}}{H_{2_{\left(Elec.\right)}}}$ (16)

$Bi{o}_{cost}=M_{bio}\times LH{V}_{bio}$ (17)

$M_{Cost}=\frac{I_{cost}\times F}{hrs\times H_{2_{\left(Elec.\right)}}}\times 0.03$ (18)

$F=\frac{k^n\times \left(k-1\right)}{k^n-1}$ (19)

$k=1+\frac{ir}{100}$ (20)

$Cos{t}_{H_2}$ = cost of hydrogen; $P{n}_{cost}$ = operations cost; $M_{Cost}$ = maintenance cost; $I_{cost}$ = initial cost is taken as $15000 [29] ; hrs = hours per year; F = annuity factor; $P{o}_{bio}$ = power of biogas; $Bi{o}_{cost}$= cost of biogas taken as $0.0518/kWh [29] ; $M_{bio}$ = mass of biogas (kg); $LH{V}_{bio}$ = biogas lower heating value taken

as 10.514 kWh/kg [34] ; n = total project period (10 years); and ir = interest rate.

A project’s economic viability is measured by its net present value (NPV); specifically, a positive net present value denotes an economically viable project, while a negative net present value denotes an economically unviable enterprise [40] . The NPV ( $P_{j_{NPV}}$) for the project was determined based on Equation (21) to Equation (25).

$P_{j_{NPV}}={\displaystyle {\sum }_{n=0}^y\frac{C_n}{{\left(R{D}_r+1\right)}^n}}=I_{cost}+\frac{C_1}{{\left(R{D}_r+1\right)}^1}+\cdots +\frac{C_y}{{\left(R{D}_r+1\right)}^n}$ (21)

$P_{j_{REV}}=Cos{t}_{H_2}\times H_{2_{\left(Q\right)}}$ (22)

$P_{j_{tax}}=Ta{x}_{\left(IPG\right)}\times P_{j_{REV}}$ (23)

$P_{j_{profit}}=P_{j_{REV}}-P_{j_{tax}}-P{n}_{cost}-M_{Cost}$ (24)

$R{D}_r=\frac{\propto +1}{I_{f_{rate}}+1}-1$ (25)

$C_n$ = net cash flows; $R{D}_r$ = annual real discount; $P_{j_{REV}}$ = revenue generated; $P_{j_{tax}}$ = tax paid by the project; $Ta{x}_{\left(IPG\right)}$ = Ghana’s tax on incomes, profits and capital [41] ; $P_{j_{profit}}$ = project profit; $I_{f_{rate}}$ = inflation rate in Ghana [42] ; $\propto$ = nominal discount [34] .

The benefit-to-cost ratio (BCR) is an indicator of profitability related to the net present value. It measures the relationship between the system’s lifetime investment costs and overall earnings [40] . The benefit-to-cost ratio is estimated based on Equation (26).

$P_{j_{BCR}}=\frac{P_{j_{NPV}}}{T_{IVC}}+1$ (26)

$P_{j_{BCR}}$ = the project BCR, $T_{IVC}$ = is the total investment cost.

In Ghana, several socioeconomic groups are forced to use generators due to inadequate state energy delivery [43] . These generators commonly supply the electricity in urban and rural areas because the utility sector cannot produce enough power to fulfill the rising electricity demand. The primary fuel source for these generators is fossil diesel, which has potential severe environmental consequences. Hydrogen gas could offset large amounts of diesel, resulting in huge cost savings. The electricity demand-supply mismatch may be resolved by replacing diesel generators with hydrogen-powered fuel cells [17] . Equation (27) was used to calculate the quantity of diesel fuel (DF) that could be offset by hydrogen-electricity produced from residues [34] .

$D_{\left(fuel\right)}=\frac{\delta \times LH{V}_{\left(hydrogen\right)}\times densit{y}_{\left(H_2\right)}\times H_{2_{\left(Q\right)}}}{D_{\left(Den\right)}\times \frac{LH{V}_{\left(D\right)}}{\gamma }\ast Ge{n}_{\left(\epsilon \right)}}$ (27)

where $D_{\left(Den\right)}$ represents diesel density which is 0.84 kg/litre [44] ; $LH{V}_{\left(D\right)}$ represents diesel LHV which is 42.5 MJ/kg [45] ; γ denotes MJ to kWh conversion factor and $Ge{n}_{\left(\epsilon \right)}$ denotes diesel generator efficiency of 33% [46] .

The release of CO₂, CH₄, and nitrous oxide (N₂O) from diesel fuel generators poses severe problems [47] . The energy industry is key to preventing irreversible climate change because it is the main generator of greenhouse gas emissions. If clean, renewable energy replaces fossil fuels, carbon emissions might significantly decrease [48] . Hydrogen-powered fuel cells have proposed a possible solution to the energy-environment gap [17] . Given this, Equation (28) to Equation (30) were used to estimate the global warming mitigation potential (GWP).

$C{O}_{2_{eq}}\left(\phi \right)=C{O}_{2_{\left(GW\right)}}\times {\stackrel{⌣}{Ж}}_{\left(C{O}_2\right)}\times D_{\left(fuel\right)}$ (28)

$C{O}_{2_{eq}}\left(\aleph \right)=N_2{O}_{\left(GW\right)}\times {\stackrel{⌣}{Ж}}_{\left(N_{2}O\right)}\times D_{\left(fuel\right)}$ (29)

$C{O}_{2_{eq}}\left(\vartheta \right)=C{H}_{4_{\left(GW\right)}}\times {\stackrel{⌣}{Ж}}_{\left(C{H}_4\right)}\times D_{\left(fuel\right)}$ (30)

The total global warming mitigation potential ( $GW{P}_{\left(T\right)}$) was estimated as:

$GW{P}_{\left(T\right)}=C{O}_{2_{eq}}\left(\phi \right)+C{O}_{2_{eq}}\left(\aleph \right)+C{O}_{2_{eq}}\left(\vartheta \right)$ (31)

where $C{O}_{2_{eq}}\left(\aleph \right)$, $C{O}_{2_{eq}}\left(\phi \right)$ and $C{O}_{2_{eq}}\left(\vartheta \right)$ are the nitrous oxide, carbon dioxide and methane CO₂ equivalents; ${\stackrel{⌣}{Ж}}_{\left(C{O}_2\right)}$, ${\stackrel{⌣}{Ж}}_{\left(N_{2}O\right)}$, ${\stackrel{⌣}{Ж}}_{\left(C{H}_4\right)}$ are diesel-specific emission factors for CO₂, N₂O and CH₄ taken as 2.7 kg/liters, 2.167 × 10⁻⁵ kg/liters and 3.612 × 10⁻⁴ kg/liters; $C{O}_{2_{\left(GW\right)}}$, $N_2{O}_{\left(GW\right)}$ and $C{H}_{4_{\left(GW\right)}}$ GWP of CO₂, N₂O, and CH₄ considered as 1 kg $C{O}_{2_{eq}}$, 32 kg $C{O}_{2_{eq}}$ and 298 kg $C{O}_{2_{eq}}$, respectively [49] [50] [51] .

The study evaluated the potential for producing purified biogas in Ghana using anaerobic digestion technology. Biogas steam reforming was used to determine the amount of hydrogen gas that could be generated. Figure 2 shows the purified biogas and hydrogen gas potential from agricultural residues. The findings indicate that 11406.03 million cubic meters (Mm³) of purified biogas were obtained within the study’s timeframe (2011-2020), with an annual potential of 1140.60 Mm³. The purified biogas potential increased from 974.80 Mm³ (2011) to 1402.05 Mm³ (2020). In addition, the residues from yam had the most purified biogas potential of 2903.12 Mm³ for the period and an annual potential of 290.31 Mm³, and maize residues had the second-highest share of 2853.21 Mm³ (2011-2020) and 285.32 Mm³ (yearly potential). For the annual share, the other residues with a significant purified biogas yield were plantain residues (196.42 Mm³),

cassava residues (144.02 Mm³), and cocoa pods (53.07 Mm³). It was found that the annual purified biogas from oil palm (16.45 Mm³), groundnuts (13.11 Mm³), and millet (12.71 Mm³) residues were not promising.

The findings showed that hydrogen production increased from 223.66 kilotons (kt) (2011) to 321.69 kt (2020). The overall output potential of hydrogen for the project is 2,617 kt. It was also discovered that the average annual production of bio-H₂ was 261.70 kt. During the period, the total bio-H₂ gas generated for the topmost residues were 666.09 kt (yam residues), 654.64 kt (maize residues), 450.66 kt (plantain residues), 330.44 kt (cassava residues), and 121.75 kt from cocoa pods. These residues contributed 66.61 kt, 65.46 kt, 45.07 kt, 33.04 kt, and 12.18 kt of bio-H₂ gas yearly. From the results, yam (25.45%) and maize (25.01%) residues produced 50.47% of the total bio-H₂. Plantain residues account for 17.22%, cassava (12.63%), and cocoa had 4.65%. The annual bio-H₂ potential for sorghum, rice, cowpea, soybeans, oil palm, and groundnut residues was 8.91 kt, 7.56 kt, 6.95 kt, 6.22 kt, 3.78 kt, and 3.01 kt. Millet residues had the most negligible contribution of 29.17 kt (1.11%) for the period and a lower annual yield of 2.92 kt. The study shows that one tonne (1000 kg) of residues could produce about 16.59 kg of bio-H₂. Table 1 shows (see column 2) the bio-H₂ gas generation capacity for a tonne of the different types of residues.

From the study, hydrogen gas was produced by biogas steam reforming, and its potential for generating energy was measured. The study demonstrated that a tonne (1000 kg) of residues could produce 29.83 kWh of electricity, while the specific energy generation potential per tonne of the residues is depicted in Table 1 (see column 3). The results of the electricity potential of bio-hydrogen are presented in Figure 3 . The study reveals that a good amount of electricity can be generated with a total capacity of 4,705.89 GWh for the period. The electricity generation capacity in 2011 was 402.18 GWh which observed a steady increase in production of 578.45 GWh in 2020. In addition, the findings show that Ghana can generate 470.59 GWh annually. Substantial electricity was produced from yam, maize, plantain, and cassava residues, with a total production for the project period of 1197.77 GWh, 1177.17 GWh, 810.38 GWh, and 594.19 GWh.

These residues had an annual electricity potential of 119.78 GWh (yam residues), 117.72 GWh (maize residues), 81.04 GWh (plantain residues), and 59.42 GWh (cassava residues). Yam and maize residues provided a promising energy potential, accounting for 50.47% of the total power. The study highlights that the total energy share of the agro-wastes for cocoa pods was 218.94 GWh, followed by sorghum (160.260 GWh), rice (135.98 GWh), cowpea (124.99 GWh), soybeans (111.79 GWh), oil palm (67.89 GWh) and groundnut (54.08 GWh), whiles millet had the least of 52.45 GWh. The annual electricity from these seven residues had a lower annual power ranging from 21.89 GWh to 5.24 GWh.

M-R = maize residues, R-R = rice residues, Sg-R = sorghum residues, Mi-R = millet residues, Sy-R = soybean residues, Gn-R = groundnut residues, Cp-R = cowpea residues, Y-R = yam residues, Cs-R = cassava residues, Pt-R = plantain residues, Op-R = oil palm residues and Cc-R = cocoa residues.

The economic assessment was based on the total bio-H₂ and electricity generated for the project period. The study shows that the total cost of operations will be $8206094949.27, with an annual cost of $820609494.93, corresponding to $1.744/kWh. The total maintenance cost is $24501036.03 with a yearly output of $2450103.60; this corresponds to $0.005/kWh. The hydrogen production cost was $816701202.71, which will have a yearly bio-H₂ cost of $81670120.27. The cost per kWh of electricity was estimated at $0.174. The project’s revenue for the 10 years is $454177067.46 and could generate a total profit of $258880926.71, leading to an annual profit margin of $25888092.67. The sum of net cash flow was estimated at $234364892.43. The project has an annual positive NPV value of $213555060.94 corresponding to $2135550609.45 (2011-2020). The positive NPV values exemplify that using residues for bio-H₂ for power generation is economically viable. Similarly, the study had a BCR value of 1.26, which is encouraging and implies it is worth investing in the project.

The diesel displacement capacity of bio-H₂ energy was determined. The results show that 142.11 million liters (ML) of diesel can be displaced annually. The study discovered that 1421.09 ML of fossil diesel consumption could be avoided during the project period, with a diesel displacement capacity of 121.45 ML in 2011 and 174.68 ML in 2020. Table 2 shows the fossil diesel that was displaced for the project period. Yam and maize residues could displace 36.17 ML and 35.55 ML per year, representing 50.47% of the total displaced diesel potential of the project.

The remaining 10 residues contribute to 49.53% of the total diesel avoided. Given this, the amount of diesel that could be displaced per year by plantain residues is 24.47 ML, with cassava residues contributing 17.94 ML. In addition, cocoa, sorghum, rice, cowpea, soybeans, oil palm, groundnut, and millet residues had an annual diesel displacement potential of 6.61 ML, 4.84 ML, 4.11 ML, 3.77 ML, 3.38 ML, 2.05 ML, 1.63 ML, and 1.58 ML. On average, a tonne of residues for H₂-power could displace 9.01 L of fossil diesel, and Figure 4 shows the quantity of diesel displaced per tonne of the specific residues. The study demonstrates that bio-H₂ electricity has environmental co-benefits, with global warming mitigation potential of 24.49 kg CO₂eq per tonne of residue. Figure 4 depicts the global warming reduction potential per tonne for all the crop residues. It was also discovered that 1 kg of H₂ could mitigate 1.48 kg CO₂eq. Within the period, 3862.55 kt CO₂eq could be avoided with an annual reduction potential of 386.26 kt CO₂eq. In addition, from 2011 to 2020, global warming mitigation increased from 330.11 kt CO₂eq to 474.79 kt CO₂eq.

It was also revealed that for the specific residues, the total global warming reduction potential for yam and maize was 983.12 kt CO₂eq and 966.21 kt CO₂eq, demonstrating that these residues could save 98.31 kt CO₂eq and 96.62 kt CO₂eq per year. Similarly, the two residues mentioned above contribute 50.47% of the total CO₂ reduction. Figure 5 highlights residues’ carbon emission reduction potential. The other residues could avoid CO₂ emissions with annual mitigation potential for plantain as 66.52 CO₂eq followed by cassava (48.77 kt CO₂eq), cocoa (17.97 kt CO₂eq), sorghum (13.15 kt CO₂eq), rice (11.16 kt CO₂eq), cowpea (10.26 kt CO₂eq), soybeans (9.18 kt CO₂eq) and oil palm (5.57 kt CO₂eq). Groundnut and millet had a CO₂ reduction potential of less than 5 kt CO₂eq each. Similarly, the total global warming reduction potential for the 10 agricultural residues was from 665.16 kt CO₂eq to 43.05 kt CO₂eq, contributing to 49.53% of the emission reduction.

The study highlights that agricultural residues offer a promising alternative for producing sustainable hydrogen. Hydrogen demand from 2020 to 2021 increased by 5%, and global demand for hydrogen in 2021 was 94 Mt [52] , indicating that the bio-H₂ produced in this study may meet 2.78% of the global demand for hydrogen. The study reveals that yam, plantain, cassava, and maize residues have a greater potential for bio-H₂. The residues with higher quantities equally had an increased bio-hydrogen generation potential [12] .

The annual bio-H₂ production (261.70 kt) from residues is close to the annual H₂ production (284.93 kt) from food waste in Lagos reported by Ayodele et al. [17] . The findings partly agree with, Asadi et al. [16] , where the grain crops residues such as maize had the greatest impact on bio-H₂. Results from the previous authors revealed that a tonne of residues could generate an average of 7.16 kg of H₂, which is lower than the H₂ potential in the current paper of 16.59 kg. This difference is attributable to the fact that the previous paper used a mathematical framework to study bio-hydrogen synthesis, whereas the current study was based on biogas steam reforming. This development proves that biogas steam reforming has higher hydrogen generation potential, and the technology can be adopted in Ghana. According to earlier research, through the biochemical generation of bio-H₂, one tonne of maize residues may generate 9.11 kg of H_2, and one tonne of rice residues can generate 7.69 kg of H₂ [53] . These values are less than the existing values of 17.81 kg H₂ (one tonne of maize residues) and 16.43 kg H₂ (one tonne of rice residues), indicating that biogas steam reforming has a greater hydrogen potential. Also, an assessment from previous research revealed that about 84.87 kg of H₂ could be generated per tonne of food waste. The significant difference is due to food waste’s higher carbohydrate and biodegradable content [34] . Based on the lignocellulosic content of residues, the value presented in this research is lower. The results align with previous research where the authors discovered that maize residues provide 20% to 28% hydrogen [54] . According to Wei et al. [55] , a low hydrogen yield was found in rice residues which share similarities with this study.

According to the Energy Commission [56] , Ghana consumed a total of 21466 GWh of electricity. Given this value, the findings show that the current power potential could displace 21.92% of the energy consumption. Compared to other agro-wastes, yam, maize, plantain, and cassava have impressive electricity generation potential and can be exploited as sustainable renewable energy resources. The results are consistent with Cudjoe et al. [34] , who confirmed H₂ (221.12 billion kg) from biomass resources (food waste) has a substantial electricity generation potential of 661.97 TWh. In contrast, an assessment of the previous paper showed 1 kg of H₂ from food wastes corresponds to 2.99 kWh, whereas the current paper reveals that 1 kg of H₂ from agricultural residues corresponds to 1.80 kWh. The variances are due to the diverse composition of the feedstocks. Based on fuel cell-hydrogen-wind technology, Acakpovi et al. [19] determined that Ghana can produce 25999 kWh annually. The value obtained by Acakpovi et al. [19] is less than the yearly power generation potential estimated by the current study, which is 470.59 GWh. This demonstrates that utilizing residues for bio-H₂ synthesis through biogas steam reforming has high electricity potential. Like others in Africa, Ghana’s economy has seen energy demand expand faster than supply [57] . Ghana aims for 10% renewable energy by 2030, and hydrogen is considered an alternative to fossil fuels [58] . Using residues to generate hydrogen keeps biomass in the technology cycle longer, forming a closed loop and promoting sustainable energy security to advance the circular bioeconomy.

The results demonstrate that the project is economically viable and will give investors some returns. The electricity cost in the current paper ($0.174/kWh) contrasts with Cudjoe et al. [34] , in which the authors reported a cost of $0.814/kWh. This could be attributable to the fact that agricultural residues were utilized as feedstock in the current investigation, whereas food wastes were used in the earlier study. This implies that using crop residues for bio-H₂ electricity is cheaper than using food wastes. According to Acakpovi et al. [19] the cost of electricity from fuel cell-hydrogen-wind technology per kWh is $0.602. The cost from the earlier research is more expensive than the current price ($0.174/kWh). This means that the technology applied in this study is cost-effective. The positive net present value values imply that investing in residues-H₂ energy generation is worthwhile. The findings concur with Lui et al. [59] , who verified that using biomass for bio-hydrogen had positive NPV in all scenarios. This shows that using residues as feedstock for biogas steam reforming to produce hydrogen will be profitable. The benefit-to-cost ratio for the study was more than one and the paper partly corresponds to Abdelhady [40] , who had a benefit-to-cost ratio greater than one (1.06). The discrepancy between the present number and the earlier value is attributable to the fact that the current study used residues, whereas the earlier paper relied on solar energy. Using crop residues for hydrogen power generation has a higher benefit-to-cost ratio and can yield more profits. When the benefit-to-cost ratio is more than one, it indicates that investment in the project will generate a profit. On the other hand, a BCR < 1 will generate a loss, and a BCR = 1 implies there will be no profit or loss. The paper reveals that biogas steam reforming is an economically viable technology that can be implemented in Ghana.

The study garnered that large amounts of diesel could be displaced by H₂ electricity, reducing pollution and cutting down costs. The displacement of fossil fuel in Ghana by using hydrogen power will be a relief, as many individuals have voiced concerns about the rising price of fossil diesel. As of 12 September 2022, the price of 1 liter of diesel in Ghana was 14.260 Ghana cedis (GS), equivalent to $1.440 [60] . This implies that for the project period, 20264.743 Ghana cedis (equivalent to $2046.360) could be saved when diesel is displaced. The findings of the fossil diesel displacement of H₂ electricity are consistent with Ayodele et al. [17] , who emphasized about 7.446 ML of diesel fuel. Similarly, the results agree with previous findings where 15482.26 ML of diesel fuel was replaced with power generated from hydrogen gas [34] .

In Ghana, the GHG emissions are estimated at 37650 kt CO₂ [61] . Compared to the CO₂ emission reduction potential of the present study, this could offset 10.26% of the total emissions in Ghana. The study exemplifies that bio-hydrogen has the potential to reduce global warming, which aligns with earlier research. The study is consistent with Alves et al. [33] , who indicated that generating hydrogen from renewable resources like biogas significantly reduces GHG emissions. Biogas steam reforming as a technology for bio-H₂ production was studied using a life cycle assessment which revealed that 5.59 kg CO₂eq could be obtained from a kg of H₂ [62] . This value is higher than the findings from the current paper because this paper only considered the emission reduction from fossil diesel. The CO₂ savings from bio-H₂ implies that the technology can positively influence the bioeconomy. Using residues for bio-H₂ electricity generation is cheaper, more profitable for investors, and significantly decreases CO₂ emissions, which aligns with the circular bioeconomy concept.

The circular bioeconomy movement unites the circular economy and bioeconomy agendas to attain sustainability [63] . Among the 2030 sustainable development goals, 12 goals are linked to the circular bioeconomy [64] . Through the current study, SDG 2 (zero hunger) can be achieved in Ghana. Farmers will benefit from improved crop yields and increased income by using digestate from biogas as fertilizer. This will ensure that food is available all year, and farmers will have enough money to purchase other foodstuffs they do not cultivate to feed their families. Food prices will be affordable when there is an excess of food in the country. Sustainable development goal 3 (good health and wellbeing) can be attained since bio-hydrogen power reduces pollution.

Additionally, the rate of burning agricultural residues will reduce, and humans and other living species will be healthier. Less land and water pollution will result in the achievement of sustainable development goal 6 (clean water and sanitation). Healthy people will not frequently visit hospitals, resulting in a drop in expenses, and people can save more money. Bioelectricity production would ensure people access cheaper, ecologically sustainable electricity, in line with SDG 7 (affordable and clean energy). Establishing bioenergy plants, particularly in regions with significant production of residues from maize, yam, plantain, and cassava will create employment opportunities which will help achieve SDG 8 (decent work and economic growth).

Bio-hydrogen is the innovative fuel of the future that will advance the creation of anaerobic digestion plants and other sectors. Establishing fertilizer and food processing plants could contribute to reaching SDG 9 (industry, innovation and infrastructure). Implementing the project will promote sustainability in the administrative areas. This will result in the sustainable production of food and energy and its consumption. SDG 11 (sustainable cities and communities) and SDG 12 (responsible consumption and production) will be accomplished. Since the project will reduce Ghana’s GHG emissions by 10.26%, it will contribute to achieving sustainable development goal 13’s carbon neutrality target (climate action). Also, both terrestrial and aquatic organisms will be safeguarded, as neither land nor water will be contaminated. Consequently, SDG 14 (life below water) and SDG 15 (life on land) will be met. In order to accomplish the sustainable development goals, the circular bioeconomy offers a systems approach to the sustainable usage of biological resources for improved production, environment, and quality of life [64] . Utilizing agricultural residues for hydrogen production will ensure the efficient use of resources. This will contribute to Ghana’s green development by promoting sustainable development by providing green energy. In light of this, the project will not only serve as a strategy for mitigating the effects of climate change but also create jobs for citizens and improve off-farm agricultural enterprises. The hydrogen market is rapidly increasing and exhibiting features of an integrated industry [7] [65] . A sustainable future can be attained by using bio-hydrogen as an alternative to fossil fuels [66] . This study serves as a strategic innovation pillar to produce electricity from hydrogen using residues which can help Ghana achieve the 2030 Sustainable development goals.